Problem 5.6b Ammonia Process - Energy Balance for Mixer into R3 Using average molar heat capacities 7.427.02Tref (K) 273.15 11.8614.57S 3 4.97323.15 Temp (K) Feed2507.98 N(N2) Feed7522.93 N(H2) Feed 735.76 Temp (K) R2 out0.00 N(NH3) Feed 4647.56 N(N2) R2 out96.54 N(CH4) Feed 12201.88 N(H2) R2 out34.55 N(Ar) Feed 3602.98 N(NH3) R2 out3649923.65 Feed 2202.26 N(CH4) R2 out477.80 N(Ar) R2 out Use Goal See to !ar" T R2 #$%%% R2 out &$er'" (ala$)e * 0 (out + ,$)50% of Feed S 5 0S 3- MixerS 6671.36 Temp (K) R3 #$ 748.77 Temp (.)5901.55 N(N2) R3 #$15963.34 N(H2) R3 #$3602.98 N(NH3) R3 #$2250.53 N(CH4) R3 #$495.07 N(Ar) R3 #$%%% R3 #$/p02/p12/p013/p/14/p2rNshs (C!)Nshs (C!)Nshs (C!)